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High Cell Density Cultivation of HEK293 Cells Using a 2L Membrane-Stirred Bioreactor
Lennart Jacobtorweihe1, Yasemin van Heuvel2, Kathrina Scheiermann2
1Max Planck Institute for Dynamics of Complex Technical Systems, Magdeburg, Germany.
Biotechnology and Bioengineering
|July 26, 2026
Summary
A novel membrane-stirrer bioreactor enables high cell density (HCD) cultivation for improved protein and virus production. This system overcomes oxygen supply and foam formation challenges in stirred tank bioreactors, achieving high cell concentrations in perfusion mode.
Area of Science:
- Biotechnology and Bioprocessing
- Cell Culture Engineering
- Recombinant Protein Production
Background:
- Perfusion systems offer advantages for continuous animal cell cultivation at high cell density (HCD), enhancing volumetric productivity and product quality.
- Conventional stirred tank bioreactors (STRs) face challenges in HCD cultivations (>50 × 10^6 cells/mL), including limited oxygen supply, CO2 stripping, high viscosity, and foam.
- Addressing these limitations is crucial for process intensification in biopharmaceutical manufacturing.
Purpose of the Study:
- To investigate a novel membrane-stirrer (MemStir) bioreactor for efficient gas transfer and HCD cultivations.
- To evaluate the MemStir system's performance in overcoming aeration and foam formation issues in perfusion cell culture.
- To assess the MemStir system's suitability for producing recombinant proteins, viruses, and viral vectors.
Main Methods:
- A novel MemStir bioreactor utilizing hollow-fiber membranes for bubble-free gas diffusion was designed and tested.
- Performance was benchmarked against shake flasks and conventional STRs in batch mode using HEK-LTV cells.
- HCD cultivations in perfusion mode were conducted using the MemStir system coupled with an alternating tangential flow system.
Main Results:
- The MemStir system achieved volumetric mass transfer coefficient (kLa) values of 10-30 h^-1, ensuring sufficient oxygen supply for HCD.
- Suspension cell growth in the MemStir system was comparable to conventional STRs, reaching a maximum viable cell concentration of 7.6 × 10^6 cells/mL in batch mode.
- In perfusion mode, HEK-LTV cells reached concentrations up to 92 × 10^6 cells/mL with a specific growth rate of 0.022 h^-1, with stable pH control and no foam formation.
Conclusions:
- The MemStir bioreactor effectively overcomes limitations in oxygen supply and foam formation associated with HCD cultivations.
- The system demonstrates robust performance in both batch and perfusion modes, supporting high cell densities for biopharmaceutical production.
- The MemStir system presents a viable and advantageous alternative for process intensification in animal cell culture.
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